WO2014097171A1 - Polythiols à titre de catalyseurs d'isomérisation cis/trans pour composés insaturés - Google Patents

Polythiols à titre de catalyseurs d'isomérisation cis/trans pour composés insaturés Download PDF

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WO2014097171A1
WO2014097171A1 PCT/IB2013/061082 IB2013061082W WO2014097171A1 WO 2014097171 A1 WO2014097171 A1 WO 2014097171A1 IB 2013061082 W IB2013061082 W IB 2013061082W WO 2014097171 A1 WO2014097171 A1 WO 2014097171A1
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isomer
unsaturated
cis
trans
carbon
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PCT/IB2013/061082
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René Tobias STEMMLER
Nadine GREINER
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Dsm Ip Assets B.V.
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Priority to EA201500647A priority Critical patent/EA028500B1/ru
Priority to US14/651,510 priority patent/US9765002B2/en
Priority to EP13828833.7A priority patent/EP2935186B1/fr
Priority to BR112015014106-4A priority patent/BR112015014106B1/pt
Priority to CN201380065876.8A priority patent/CN104884419B/zh
Priority to JP2015547263A priority patent/JP6442782B2/ja
Publication of WO2014097171A1 publication Critical patent/WO2014097171A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D319/00—Heterocyclic compounds containing six-membered rings having two oxygen atoms as the only ring hetero atoms
    • C07D319/04—1,3-Dioxanes; Hydrogenated 1,3-dioxanes
    • C07D319/06—1,3-Dioxanes; Hydrogenated 1,3-dioxanes not condensed with other rings
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C43/00—Ethers; Compounds having groups, groups or groups
    • C07C43/30—Compounds having groups
    • C07C43/313—Compounds having groups containing halogen
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0215—Sulfur-containing compounds
    • B01J31/0217—Mercaptans or thiols
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C321/00—Thiols, sulfides, hydropolysulfides or polysulfides
    • C07C321/24—Thiols, sulfides, hydropolysulfides, or polysulfides having thio groups bound to carbon atoms of six-membered aromatic rings
    • C07C321/28—Sulfides, hydropolysulfides, or polysulfides having thio groups bound to carbon atoms of six-membered aromatic rings
    • C07C321/30—Sulfides having the sulfur atom of at least one thio group bound to two carbon atoms of six-membered aromatic rings
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/60—Preparation of compounds having groups or groups
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/67—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/78—Separation; Purification; Stabilisation; Use of additives
    • C07C45/81—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
    • C07C45/82—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/50—Redistribution or isomerisation reactions of C-C, C=C or C-C triple bonds
    • B01J2231/52—Isomerisation reactions
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B2200/00—Indexing scheme relating to specific properties of organic compounds
    • C07B2200/09—Geometrical isomers

Definitions

  • the present invention relates to the cis/trans isomerization of unsaturated compounds.
  • the problem to be solved by the present invention is to offer a process of isomerization and an isomerization catalyst which is very efficient, respectively, for compounds being selected from the group consisting of unsaturated ketones, unsaturated ketals, unsaturated aldehydes, unsaturated acetals, unsaturated carboxylic acids, esters of an unsaturated carboxylic acid and amides of an unsaturated carboxylic acid.
  • step b) adding a polythiol to the cis or trans isomer of the unsaturated compound A of step a);
  • Substance names starting with "poly” such as polythiol as used in the present document refer to substances formally containing two or more of the corresponding functional groups per molecule.
  • a "Cx-y-alkyl” group is an alkyl group comprising x to y carbon atoms, i.e., for example, a Ci-3-alkyl group is an alkyl group comprising 1 to 3 carbon atoms.
  • the alkyl group can be linear or branched. For example -CH(CH3)-CH2-CH3 is considered as a C 4 -alkyl group.
  • aromatic polythiol is a polythiol which has two or more SH groups being bound directly to an aromatic hydrocarbon.
  • a "phenolic alcohol” means in this document an alcohol which has a hydroxyl group which is bound directly to an aromatic group.
  • a carbon-carbon double bond is defined as being "prochiral” if addition of molecular hydrogen to said carbon-carbon double bond leads to the formation of a stereogenic carbon centre.
  • Cis/trans isomers are configurational isomers having different orientation at the double bond.
  • the term “cis” is equivalently used for “Z” and vice versa as well as “trans” for ⁇ ” and vice versa. Therefore, for example the term “cis/trans isomerization catalyst” is equivalent to the term ⁇ / ⁇ isomerization catalyst".
  • a “cis/trans isomerization catalyst” is a catalyst which is able to isomerize a cis isomer (Z-isomer) to a cis/trans isomer mixture (E/Z isomer mixture) or to isomerize a trans isomer (E-isomer) to a cis/trans isomer (E/Z isomer mixture).
  • E/Z E/Z
  • cis/trans cis/trans
  • R/S R/S
  • An "equilibrium cis/trans ratio" is the ratio of a specific couple of cis and trans isomer which is achieved as a result of submitting either said cis or trans isomer to an isomerization using the process of this invention for an extended time, i.e. until no further change of the cis/trans ratio can be observed in time.
  • Each pair of cis/trans isomers has a different equilibrium cis/trans ratio.
  • a “non-equilibrium cis/trans ratio” is any ratio of cis to trans isomer which differs from the "equilibrium cis/trans ratio”.
  • An "unsaturated" compound, ketone, ketal, aldehyde, acetal, carboxylic acid, ester of an unsaturated carboxylic acid or amide of an unsaturated carboxylic acid is defined as to be a ketone, aldehyde, ketal, aldehyde, acetal, carboxylic acid, ester of an unsaturated carboxylic acid or amide of an unsaturated carboxylic acid which is olefinically unsaturated, i.e. that it has at least one carbon-carbon double bond in its chemical structure, and which preferably has at least one prochiral carbon-carbon double bond.
  • any single dotted line represents the bond by which a substituent is bound to the rest of a molecule.
  • the unsaturated compound A selected from the group consisting of unsaturated ketones, unsaturated ketals, unsaturated aldehydes, unsaturated acetals, unsaturated carboxylic acids, esters of an unsaturated carboxylic acid and amides of an unsaturated carboxylic acid, has at least one carbon-carbon double bond in its chemical structure and preferably has at least one prochiral carbon- carbon double bond.
  • It may have more than 1 prochiral carbon-carbon double bonds and/or 1 or more non-prochiral carbon-carbon double bond(s).
  • the unsaturated compound A is of formula (l-OA) or (l-OB) or (l-OC) or (l-OD) or (l-OE) or (l-OF)
  • R' stands for a linear or a cycloaliphatic hydrocarbyl group which optionally contains additional carbon-carbon double bond(s) and Q' stands for a group selected of the group consisting of
  • Q 1 and Q 2 stand for a C 1 -C 10 alkyl group or a halogenated C 1 -C 10 alkyl group; Ci- C 4 -alkyl group or form together a C 2 -C6 alkylene group or a C6-Cs cycloalkylene group together;
  • R" stands for a CrC 4 -alkyl group, particularly for a methyl or ethyl group; and R'" stands for H or a CrC 4 -alkyl group, particularly for a methyl or ethyl group; and where a wavy line represents a carbon-carbon bond which is linked to the adjacent carbon-carbon double bond so as to have said carbon-carbon double bond either in the Z or in the E-configuration;
  • double bond having dotted lines ( ) in formula (l-OB) or (l-OD) or (l-OF) represent either a single carbon-carbon bond or a double carbon- carbon bond.
  • the unsaturated compound A is an unsaturated ketone or unsaturated ketal or an unsaturated aldehyde or an unsaturated acetal.
  • the unsaturated compound A is an unsaturated ketone or ketal thereof or an unsaturated aldehyde or acetal thereof and has a carbon-carbon double bond in the ⁇ , ⁇ position relative to the carbonyl group.
  • the unsaturated compound A is an unsaturated ketone or ketal thereof or an unsaturated aldehyde or acetal thereof and has a carbon-carbon double bond in the ⁇ , ⁇ position relative to the carbonyl group and has a carbon-carbon double bond in the ⁇ , ⁇ position relative to the carbonyl group.
  • unsaturated ketones or aldehydes have the formula (II).
  • the unsaturated ketone or aldehyde is selected from the group consisting of 3,7-dimethylocta-2,6-dienal, 3,7-dimethyloct-2-enal, 6,10- dimethylundeca-3,5,9-trien-2-one, 6, 10-dimethylundeca-5,9-dien-2-one, 6, 10- dimethylundec-5-en-2-one, 6,10-dimethylundec-3-en-2-one, 6,10-dimethylundec- 3,5-diene-2-one, (R)-6, 10-dimethylundec-3-en-2-one, 6,10, 14-trimethylpentadeca- 5,9, 13-trien-2-one, 6,10, 14-trimethylpentadeca-5,9-dien-2-one, 6, 10, 14- trimethylpentadec-5-en-2-one and (R)-6, 10, 14-trimethyl
  • the unsaturated ketone or aldehyde is a ketone.
  • the unsaturated compound A is a ketal or acetal of an unsaturated ketone or unsaturated aldehyde, particularly an acetal or a ketal of formula (I) or (II).
  • the ketal of an unsaturated ketone can be preferably formed from the above mentioned unsaturated ketone and an alcohol.
  • the acetal of an unsaturated aldehyde can be formed from the above mentioned unsaturated aldehyde and an alcohol.
  • the alcohol used for the ketal or acetal formation can, principally, be any alcohol, i.e. the alcohol may comprise one or more hydroxyl groups.
  • the alcohol may be a phenolic alcohol or an aliphatic or cycloaliphatic alcohol.
  • the alcohol is preferably an alcohol which has 1 to 12 carbon atoms.
  • the alcohol having one hydroxyl group is selected from the group consisting of methanol, ethanol, 1- propanol, 2-propanol, 1-butanol, 2-methyl-1-propanol, 2-butanol, pentane-1-ol, 3- methylbutane-1-ol, 2-methylbutane-1-ol, 2,2-dimethylpropan-1-ol, pentane-3-ol, pentane-2-ol, 3-methylbutane-2-ol, 2-methylbutan-2-ol, hexane-1-ol, hexane-2-ol, hexane-3-ol, 2-methyl-1-pentanol, 3-methyl-1-pentanol, 4-methyl-1-pentanol, 3- methyl-2-pentanol, 4-methyl-1-pentanol, 3- methyl-2-pentanol, 4-methyl-2-pentano
  • primary or secondary alcohols are used as alcohols with one hydroxyl group.
  • primary alcohols are used as alcohols with one hydroxyl group.
  • methanol, ethanol, 1-propanol, 2-propanol, 1- butanol, 2-butanol or 2,2,2-trifluoroethanol preferably methanol, ethanol, 1- propanol, 1-butanol or 2,2,2-trifluoroethanol, are used as alcohols with one hydroxyl group.
  • the alcohol is a diol.
  • the diol is selected from the group consisting of ethane-1 ,2-diol, propane-1 ,2-diol, propane-1 ,3-diol, butane-1 ,4-diol, butane-1 ,3-diol, butane-1 ,2-diol, butane-2,3-diol, 2- methylpropane-1 ,2-diol, 2-methylpropane-1 ,3-diol, 2,2-dimethylpropane-1 ,3-diol, 1 ,2-dimethylpropane-1 ,3-diol, 3-methylpentane-2,4-diol and 2- (hydroxymethyl)cyclohexanol, benzene-1 ,2-diol and cyclohexane-1 ,2-diols. From two cyclohexane-1 ,2-diols, propane-1
  • the two hydroxyl groups are in one embodiment bound to two adjacent carbon atoms, hence these diols are vicinal diols.
  • Vicinal diols form a 5 membered ring in a ketal or acetal.
  • Particularly suitable are vicinal diols which are selected from the group consisting of ethane-1 ,2-diol, propane-1 ,2-diol, butane-1 ,2-diol, butane-2,3-diol, 2- methylpropane-1 ,2-diol, benzene-1 ,2-diol and syn-cyclohexane-1 ,2-diol, particularly ethane-1 ,2-diol.
  • diols in which the hydroxyl groups are separated by 3 carbon atoms, and, hence, form a very stable 6 membered ring in a ketal or acetal.
  • diols of this type are propane-1 ,3-diol, butane-1 ,3-diol, 2-methylpropane-1 ,3-diol, 2-methylbutane-1 ,3-diol, 2,2-dimethyl- propane-1 ,3-diol, 1 ,2-dimethylpropane-1 ,3-diol, 3-methylpentane-2,4-diol and 2- (hydroxymethyl)cyclohexanol.
  • Preferably primary alcohols are used as diols.
  • reaction conditions and stoichiometry used for the acetal or ketal formation are known to the person skilled in the art. Particularly the acetal or ketal is formed under the influence of an acid.
  • Q 1 and Q 2 stand either individually both for a C1-C10 alkyl group or a halogenated C1-C10 alkyl group;
  • Q 1 and Q 2 stand particularly for
  • Q 3 , Q 4 , Q 5 and Q 6 are independently from each other hydrogen atoms or methyl or ethyl groups.
  • the ketal or the acetal of formula (XI) or (XII) are (E)-2-(4,8- dimethylnona-3,7-dien-1-yl)-2,5,5-trimethyl-1 ,3-dioxane, (E)-2,6-dimethyl-10, 10- bis(2,2,2-trifluoroethoxy)undeca-2,6-diene, (E)-2-(4,8-dimethylnon-3-en-1-yl)- 2,5,5-trimethyl-1 ,3-dioxane, (E)-6, 10-dimethyl-2,2-bis(2,2,2-trifluoroethoxy)undec- 5-ene, (E)-2,5,5-trimethyl-2-(4,8,12-trimethyltridec-3-en-1-yl)-1 ,3-dioxane, (R,E)- 2,5,5-trimethyl-2-(4,8,12-trimethyltridec-3-en-1-yl)-1 ,3
  • step a) a cis or a trans isomer of an unsaturated compound A is provided.
  • only one single stereoisomer of the compound A is provided.
  • Such a single stereoisomer of compound A may be a result of a stereospecific synthesis or of a separation process of stereoisomers.
  • the cis or a trans isomer of a unsaturated compound A is provided as a mixture of cis and trans isomers in a non-equilibrium cis/trans ratio.
  • a non-equilibrium cis/trans ratio is larger than 70/30, preferably larger than 80/20, more preferably larger than 90/10 or smaller than 30/70, preferably smaller than 20/80, more preferably smaller than 10/90.
  • step b) a polythiol is added to the cis or trans isomer of the unsaturated compound A of step a);
  • the polythiol is a cis/trans isomerization catalyst which isomerizes the carbon carbon double bond(s).
  • polythiols are aromatic polythiols or polythiols of formula (X)
  • n1 represents an integer from 1 to 4, particularly 2,
  • ml represents an integer from 2 to 8, particularly 3 or 4, preferably 4; and A represents an aliphatic m1-valent hydrocarbon group of the molecular weight of between 28 g/mol and 400 g/mol, particularly between 90 and 150 g/mol.
  • a first group of preferred polythiols are aromatic polythiols.
  • the SH groups are bound directly on an aromatic hydrocarbon.
  • the aromatic hydrocarbon may have one or several aromatic rings.
  • the aromatic rings can form a fused ring system or can be separated by spacers for example by alkylene groups or by functional groups.
  • the SH groups may be bound directly on a the same aromatic ring or on different aromatic rings.
  • aromatic polythiols are 4,4'-dimercaptobiphenyl or 4,4'-thiodibenzenethiol.
  • a further group of preferred polythiols are polythiols of formula (X). These substances are esters of a polyol A(OH) m i and a carboxylic acid having a terminal mercapto group SH-(CH 2 ) n i-COOH.
  • the preferred polyols A(OH) m i having a molecular weight of between 62 and 538 are
  • esters can be prepared by different methods, not limited of a reaction of the polyol with the above mentioned carboxylic acid having a terminal mercapto group.
  • polythiols pentaerythritol tetra(mercaptoacetate), trimethylolpropane tris(mercaptoacetate), glycol dimercaptoacetate, pentaerythritol tetra-(3- mercaptopropionate), trimethylolpropanetri-(3-mercaptopropionate)( 2-ethyl-2- (((3-mercaptopropanoyl)oxy)methyl)propane-1 ,3-diyl bis(3-mercaptopropanoate)) and glycol di-(3-mercaptopropionate) have been shown to be highly preferred polythiols of formula (X) and are the preferred polythiols of all the above mentioned polythiols.
  • polythiols of formula (X) as cis/trans isomerization catalysts is very advantageous in that polythiols have generally very low vapor pressures (i.e. high boiling points) allowing them to be used at elevated temperatures, e.g. while distilling the low boiling isomer. Furthermore, the polythiols bear a high density of thiol-functionalities per molecular weight, which is very advantageous, in that only little catalyst needs to be added.
  • the use of polythiol as cis/trans isomerization catalysts is very advantageous as they allow a very fast isomerization.
  • the amount of a polythiol added to the cis or trans isomer of the unsaturated compound A is preferably between 1 and 20 %, particularly between 3 and 5 %, by weight in relation to the amount of the unsaturated compound A.
  • the molar ratio of polythiol and the unsaturated compound A is between 1 / 100 and 20 / 100, particularly between 1 / 100 and 4 / 100.
  • the way of adding of the polythiol to the unsaturated compound A is uncritical and can be done as needed. It can be added before or during step c).
  • step c) the mixture of polythiol and cis or trans isomer of the unsaturated compound A is heated to a temperature of between 20°C and the boiling point of the unsaturated compound A, particularly between 50 °C and the boiling point of the unsaturated compound A.
  • the "boiling point of the unsaturated compound A" is defined as being the boiling point of the lowest boiling cis or trans isomers being formed by the process.
  • polar solvents such as amides, pyrrolidones, sulfones, sulfoxides, ionic liquids, particularly N,N- dimethylformide (DMF) or N-methyl-2-pyrrolidone (NMP), sulfolane, dimethylsulfoxide (DMSO) and 1-butyl-3-methylimidazolium bromide has an accelarating effect on the isomerization .
  • a polar solvent particularly a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP), sulfolane and dimethylsulfoxide (DMSO).
  • a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP), sulfolane and dimethylsulfoxide (DMSO).
  • a polar solvent particularly a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP) and dimethylsulfoxide (DMSO).
  • a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP) and dimethylsulfoxide (DMSO).
  • the isomerization of a cis or of a trans isomer of an unsaturated compound A is very interesting because very often one of the isomers is the isomer of interest.
  • the cis and trans isomers mostly have different properties. For example core properties of interest such as odour or reactivity in specific chemical reactions is strongly different for the trans as compared to the cis isomer.
  • the method of isomerization and isolation in an optimal way, it even can be achieved that essentially all of the undesired isomer(s) can be transformed into the desired isomer(s) starting from a undesired isomer or a mixture of desired and undesired cis/trans isomers. More details for this possibility are given later in this document.
  • the invention in a further aspect relates to a process of producing a specific cis isomer, respectively a specific trans isomer, of an unsaturated compound A being selected from the group consisting of unsaturated ketones, unsaturated ketals, unsaturated aldehydes, unsaturated acetals, unsaturated carboxylic acids, esters of an unsaturated carboxylic acid and amides of an unsaturated carboxylic acid from a mixture of cis and trans isomers thereof comprising the steps
  • step iv) distilling off the isomer //t> p and collecting the isomer ln, p; v) cis/trans isomerization of the isomer(s) l hbp having a higher boiling point than the isomer / /& ⁇ in the presence of the polythiol being added in step ii); wherein after the step v) the steps iii) and iv) and v) are repeated subsequently
  • weight w cis and weight w trans are each 0 gram to 10 tons, with the proviso that the ratio of w cis and w trans is larger than 70/30 or smaller than 30/70 with the proviso that not both w cis and w trans are 0 grams.
  • a mixture of cis isomer(s) in an amount of weight w cis and of trans isomer(s) in an amount of weight w trans of the unsaturated compound A is provided in step i). Because the weight w cis of the cis isomer(s) or the weight w trans of the trans isomer(s) is 0 grams to 10 tons with the proviso that not both Was and Wtmns are 0 grams, a "mixture" in this context applies also to a single stereoisomer and not only to real isomer mixtures.
  • both weight w cis and weight w trans are different from 0 grams, so that in the mixture provided in step i) the cis and trans isomer(s) of the unsaturated compound A are both physically present.
  • the isomer of interest i.e. the desired isomer
  • the isomer Imp which is the isomer having the lowest boiling point of the mixture of the cis/trans isomers provided in step i).
  • the distillation is made by using specific distillation techniques assuring that impurities by other isomers are as little as - Im possible. This particularly is also achieved in that only a part, namely the purest fractions, of the desired isomer is collected in a distillation whereas a remainder is left in the distillation flask
  • the isomer(s) l bbp having a higher boiling point than the isomer li bp are cis/trans isomerized in the presence of the polythiol (being added in step ii) in step v).
  • step iv) where only a part of the isomer(s) li bp are distilled and collected in step iv) the remainder of the distillation comprises still isomer(s) li bp .
  • step v) the cis/trans isomerization is done of the remainder of the distillation.
  • the isomer(s) l hbp and/or the remainder of the distillation is either isomerized continuously or batchwise isomerized in the presence of the polythiol.
  • the system adjusts according to Le Chatelier's principle and searches to achieve the equilibrium cis/trans ratio by transforming (i.e. isomerizing) the non-desired isomer into the desired isomer facilitated by the polythiol, the cis/trans isomerization catalyst.
  • step v) By repeating the steps steps iii) and iv) and v) after step v) subsequently it is assured that the yield is increased.
  • the overall yield in the desired isomer isomer l ibp is heavily depending on the number of repetitions and/or the separation efficiency by the distillation.
  • the process leads to a net transformation of the undesired isomer to the desired isomer, which means in other words, that the weight of the collected isomer l ibp is
  • the cis isomer(s) when in the original mixture of cis and trans isomers of the unsaturated compound A provided in step a) the cis isomer(s) has a weight w c/s and the trans isomer(s) has a weight w tra ns- As discussed, principally essentially all of the undesired isomer can be transformed into the desired isomer.
  • the weight of the collected isomer li bp isomer is more than 80 % by weight, preferably more than 90 % by weight, of the sum of Wtrans and W c i s .
  • the invention in a further aspect relates to a process of producing a specific cis isomer, respectively a specific trans isomer, of an unsaturated compound A being selected from the group consisting of unsaturated ketones, unsaturated ketals, unsaturated aldehydes, unsaturated acetals, unsaturated carboxylic acids, esters of an unsaturated carboxylic acid and amides of an unsaturated carboxylic acid from a mixture of cis and trans isomers thereof comprising the steps
  • step f) cis/trans isomerization of the isomer(s) l ibp and the remainder of step e) in case there is a remainder after step e) in the presence of polythiol being added in step b); wherein after the step f) the steps c) and d) and e) and f) are repeated subsequently and wherein the weight of the collected isomer //,& is more than w cis in case the collected isomer l hbp is a cis isomer of said unsaturated compound A;
  • weight w c i s and weight w tra ns are each 0 gram to 10 tons, with the proviso that the ratio of w c / s and w tra ns is larger than 70/30 or smaller than 30/70 with the proviso that not both w c is and w tra ns are 0 grams.
  • a mixture of cis isomer(s) in an amount of weight w c i s and of trans isomer(s) in an amount of weight w trans of the unsaturated compound A is provided in step a).
  • weight w cis of the cis isomer(s) or the weight of the Wtmns of the trans isomer(s) is in 0 grams to 10 tons with the proviso that not both Was and w trans are 0 grams, a "mixture" in this context applies also to a single stereoisomer and not only to real isomer mixtures.
  • both weight w cis and weight w trans are different from 0 grams, so that in the mixture provided in step a) the cis and trans isomer(s) of the unsaturated compound A are both physically present.
  • the isomer of interest i.e. the desired isomer l hbp which has a higher boiling point than the isomer which is the isomer having the lowest boiling point of the mixture of the cis/trans isomers provided in step a).
  • the isolation of the separation specific isomer lhbp is preferably done by specific distillation techniques, for example using a side take-off point at a rectification column and eventually further rectification of the material collected at said side take-off, such as the technique and equipment that has been disclosed for example in EP 2 269 998 A2, particularly figure 1 and 3, the entire content of which is hereby incorporated by reference.
  • specific distillation techniques for example using a side take-off point at a rectification column and eventually further rectification of the material collected at said side take-off, such as the technique and equipment that has been disclosed for example in EP 2 269 998 A2, particularly figure 1 and 3, the entire content of which is hereby incorporated by reference.
  • the distillation in step d) and e) are made by using specific distillation techniques assuring that impurities by other isomers are as little as possible.
  • step f) the isomer(s) li bp and the remainder of step e) in case there is a remainder after step e) is isomerized in the presence of polythiol being added in step b).
  • the remainder of the distillation comprises still isomer(s) l hbp .
  • the isomer l ibp and the remainder of step e) are either isomerized continuously or batchwise in the presence of the polythiol. As by removal of desired product the remainder of the distillation is enriched in the undesired isomer to a non-equilibrium cis/trans ratio, the system adjusts according to Le Chatelier's principle and searches to achieve the equilibrium cis/trans ratio by transforming (i.e. isomerizing) the non-desired isomer into the desired isomer facilitated by the polythiol, the cis/trans isomerization catalyst. By repeating the steps steps c) and d) and e) and f) after step f) subsequently it is assured that the yield is increased.
  • the overall yield in the desired isomer isomer l hbp is heavily depending on the number of repetitions and/or the separation efficiency by the distillation.
  • the process leads to a net transformation of the undesired isomer to the desired isomer, which means in other words, that the weight of the collected isomer l hb ' ⁇ s
  • the collected isomer l bbp is a trans isomer of said unsaturated compound A; when in the original mixture of cis and trans isomers of the unsaturated compound A provided in step a) the cis isomer(s) has a weight w c / s and the trans isomer(s) has a weight w tra ns-
  • the weight of the collected isomer Ihbp isomer is more than 80 % by weight, preferably more than 90 % by weight, of the sum of
  • the amount of polythiol is between 1 and 20 % by weight, particulalrly betweem 3 and 5 % by weight, in relation to the amount of the unsaturated compound A.
  • the molar ratio of the polythiol and the unsaturated compound A is between 1 / 100 and 20 / 100, particularly between 1 / 100 and 4 / 100. It further has been observed that addition of polar solvents such as amides, pyrrolidones, sulfones, sulfoxides, ionic liquids, particularly N, N- dimethylformide (DM F) or N-methyl-2-pyrrolidone (NMP), sulfolane, dimethylsulfoxide (DMSO) and 1 -butyl-3-methylimidazolium bromide has an accelarating effect on the isomerization .
  • polar solvents such as amides, pyrrolidones, sulfones, sulfoxides, ionic liquids, particularly N, N- dimethylformide (DM F) or N-methyl-2-pyrrolidone (NMP), sulfolane, dimethylsulfoxide (DMSO) and 1
  • a polar solvent particularly a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP), sulfolane and dimethylsulfoxide (DMSO).
  • a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP), sulfolane and dimethylsulfoxide (DMSO).
  • a polar solvent particularly a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP) and dimethylsulfoxide (DMSO).
  • a polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3- methylimidazolium bromide, ⁇ , ⁇ -dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP) and dimethylsulfoxide (DMSO).
  • the polythiol is of formula (X), as has been described before in detail.
  • composition comprising
  • said composition further comprises at least one polar solvent, particularly at least one polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3-methylimidazolium bromide, N,N- dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP), sulfolane and dimethylsulfoxide (DMSO).
  • ionic liquids particularly 1-butyl-3-methylimidazolium bromide, N,N- dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP), sulfolane and dimethylsulfoxide (DMSO).
  • composition further comprises at least one polar solvent, particularly at least one polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3-methylimidazolium bromide, N,N- dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP) and dimethylsulfoxide (DMSO).
  • polar solvent particularly at least one polar solvent which is selected from the group consisting of ionic liquids, particularly 1-butyl-3-methylimidazolium bromide, N,N- dimethylformide (DMF), N-methyl-2-pyrrolidone (NMP) and dimethylsulfoxide (DMSO).
  • the invention relates to a ketal or acetal which is selected from the group consisting of 2-(4,8-dimethylnona-3,7-dien-1-yl)-2,5,5- trimethyl-1 ,3-dioxane, 2,6-dimethyl-10, 10-bis(2,2,2-trifluoroethoxy)undeca-2,6- diene, 2-(4,8-dimethylnon-3-en-1-yl)-2,5,5-trimethyl-1 ,3-dioxane, 6,10-dimethyl-
  • ketals and acetals are particularly suited for being isomerized according to the process of the invention.
  • the invention relates to the use of a polythiol as catalyst for the cis/trans isomerization of an unsaturated compound A which is selected from the group consisting of unsaturated ketones, unsaturated ketals, unsaturated aldehydes, unsaturated acetals, unsaturated carboxylic acids, esters of an unsaturated carboxylic acid and amides of an unsaturated carboxylic acid.
  • unsaturated compound A which is selected from the group consisting of unsaturated ketones, unsaturated ketals, unsaturated aldehydes, unsaturated acetals, unsaturated carboxylic acids, esters of an unsaturated carboxylic acid and amides of an unsaturated carboxylic acid.
  • the present invention is further illustrated by the following experiments.
  • the catalysts of table 1 were added to the E or Z isomer in an amount of 5 % by weight (concentration related to ketone). Then the mixture was stirred and heated up to 140°C under argon under which conditions isomerization took place. The amount of E and Z isomers was measured by GC regularly after certain reaction times.
  • Figure 1a shows the result of these isomerization experiments.
  • the x- axis represents the time of heating, i.e. time of isomerization at 140°C
  • the y- axis represents the percentage of E-isomer of the sum of isomers (E/(E+Z)) measured in the sample.
  • E/(E+Z) value 80% represents a E/Z ratio of 80:20.
  • Figure 1 a) shows that all catalysts induce an isomerization, i.e. the curves decrease in the case of the E-isomer with time and increase in case of the Z-isomer in time.
  • FIG 1 a) further shows that the polythiols (examples 1 and 2 (solid line) lead to much faster isomerization than the monothiols (Examples Ref.1 to Ref.6 (dashed lines)).
  • Figure 1a) also shows that the equilibrium cis/trans ratio of 6, 10-dimethylundeca-5,9-dien-2-one is between 60 and 65 % E/(E+Z).
  • Figure 1 b) shows the stability behaviour.
  • the x-axis represents again the time of heating, i.e. time of isomerization at 140°C, and the y-axis represents the purity ("P" in %) of the isomers to be isomerized and is measured by GC. Deviation from 100 % means that one or more side products have been formed.
  • Figure 1 b) shows that the polythiols have significantly better stability behaviour than the monothiols.
  • Figure 2a shows the result of this isomerization experiments.
  • the x-axis represents the time of heating, i.e. time of isomerization at 140°C
  • the y-axis represents the percentage of E-isomer of the sum of isomers (E/(E+Z)) measured in the sample.
  • E/(E+Z) value 80% represents a E/Z ratio of 80:20.
  • Figure 2a) shows the effect of different concentrations of polythiols: 1 % ("3 (1 %)"), 3 % ("3%)") and 5 % ("3 (5%)").
  • the isomerization rate depends on the concentration used.
  • FIG. 2a illustrates that that the equilibrium cis/trans ratio of 6, 10-dimethylundec-5-en-2-one is at about 65 % E/(E+Z).
  • the isomers of 6, 10-dimethylundec-5-en-2- one have been separated by distillation.
  • the E-isomer has been isolated as having a content of (E)-6, 10-dimethylundec-5-en-2-one of 95.3 % (determined by GC) and the Z-isomer has been isolated in an enriched fraction having a content of (Z)-6, 10-dimethylundec-5-en-2-one of 75.8% and a content of (E)-6, 10- dimethylundeca-5,9-dien-2-one of 23.4% (total 99.2% isomers, determined by GC).
  • Figure 3a shows the result of these isomerization experiments.
  • the x- axis represents the time of heating, i.e. time of isomerization at 140°C
  • the y- axis represents the percentage of E-isomer of the sum of isomers (E/(E+Z)) measured in the sample.
  • E/(E+Z) value 80% represents a E/Z ratio of 80:20.
  • Figure 3a) shows that the equilibrium cis/trans ratio of 6, 10- dimethylundec-5-en-2-one is between 60 and 70 % E/(E+Z).
  • Figures 4a) - c) show the result of these isomerization experiments.
  • the x-axis represents the time of heating, i.e. time of isomerization at 90°C
  • the y- axis represents the percentage of E-isomer of the sum of isomers (E/(E+Z)) measured in the sample.
  • E/(E+Z) value of 80% represents a E/Z ratio of 80:20.
  • Figure 4a) shows the accelerating effect of DMF onto the rate of isomerization.
  • Figure 4b) shows the accelerating effect of 1-butyl-3- methylimidazolium bromide, an ionic liquid, onto the rate of isomerization.
  • Figure 4c) shows the accelerating effect of DMSO onto the rate of isomerization.
  • Figures 5a)-c) show the result of this isomerization experiment.
  • the x-axis represents the time of heating, i.e. time of isomerization at 105°C
  • the y-axis represents in figure 5a) the weight ratio of ZZ/(ZZ+EZ+ZE+EE).
  • the y-axis represents in figure 5b) the weight ratio of (EZ+ZE)/(ZZ+EZ+ZE+EE).
  • the y-axis represents in figure 5c) the weight ratio of EE/(ZZ+EZ+ZE+EE).
  • Figures 5a)-c) show that all isomers are isomerized furnishing a ratio of isomers of about 40% ZZ/(ZZ+EZ+ZE+EE), about 46% (EZ+ZE)/(ZZ+EZ+ZE+EE) and about 14% EE/(ZZ+EZ+ZE+EE).
  • the isomers of 6, 10, 14- trimethylpentadeca-5,9-dien-2-one have been separated by distillation.
  • the mixture of EZ- and ZE-isomers has been isolated as having a content of 93.3% of the sum of (5E.9Z)- and (5Z,9E)-6, 10,14-trimethylpentadeca-5,9-dien-2-one, 3.0% (5E.9E)- 6,10, 14-trimethylpentadeca-5,9-dien-2-one and 1.0 % of (5Z,9Z)-6, 10, 14- trimethylpentadeca-5,9-dien-2-one (total of 97.3% 6,10, 14-trimethylpentadeca-5,9- dien-2-one isomers, measured by GC).
  • Figures 6a)-c) show the result of this isomerization experiment.
  • the x-axis represents the time of heating, i.e. time of isomerization at 90°C
  • the y-axis represents in figure 6a) the weight ratio of ZZ/(ZZ+EZ+ZE+EE).
  • the y-axis represents in figure 6b) the weight ratio of (EZ+ZE)/(ZZ+EZ+ZE+EE).
  • the y-axis represents in figure 6c) the weight ratio of EE/(ZZ+EZ+ZE+EE).
  • Figures 6a)-c) show that all isomers are isomerized and an equilibrium is approached of about 15 % ZZ/(ZZ+EZ+ZE+EE), about 54 % (EZ+ZE)/(ZZ+EZ+ZE+EE) and about 31 % EE/(ZZ+EZ+ZE+EE).

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Abstract

Cette invention concerne un procédé d'isomérisation cis/trans d'un composé insaturé A choisi dans le groupe constitué par les cétones insaturées, les cétals insaturés, les aldéhydes insaturés, les acétals insaturés, les acides carboxyliques insaturés, les esters et les amides d'un acide carboxylique insaturé faisant appel à un polythiol à titre de catalyseur d'isomérisation cis/trans. D'après les observations, l'isomérisation est très efficace et rapide.
PCT/IB2013/061082 2012-12-18 2013-12-18 Polythiols à titre de catalyseurs d'isomérisation cis/trans pour composés insaturés WO2014097171A1 (fr)

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EA201500647A EA028500B1 (ru) 2012-12-18 2013-12-18 Политиолы в качестве катализаторов цис/транс-изомеризации ненасыщенных соединений
US14/651,510 US9765002B2 (en) 2012-12-18 2013-12-18 Polythiols as cis/trans isomerization catalysts for unsaturated compounds
EP13828833.7A EP2935186B1 (fr) 2012-12-18 2013-12-18 Polythiols comme catalyseurs d'isomérisation cis/trans pour composés insaturés
BR112015014106-4A BR112015014106B1 (pt) 2012-12-18 2013-12-18 processo de uma isomerização cis/trans de um composto insaturado, processos de produção de isômeros cis e trans, composição, cetal ou acetal e uso de um politiol
CN201380065876.8A CN104884419B (zh) 2012-12-18 2013-12-18 聚硫醇作为不饱和化合物的顺式/反式异构化催化剂
JP2015547263A JP6442782B2 (ja) 2012-12-18 2013-12-18 不飽和化合物のためのシス／トランス異性化触媒としてのポリチオール

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JP6582324B2 (ja) * 2012-12-18 2019-10-02 ディーエスエム アイピー アセッツ ビー．ブイ．Ｄｓｍ Ｉｐ Ａｓｓｅｔｓ Ｂ．Ｖ． ６，１０，１４−トリメチルペンタデカ−５，９，１３−トリエン−２−オンまたは６，１０，１４−トリメチルペンタデカ−５，９−ジエン−２−オンから調製した（６ｒ，１０ｒ）−６，１０，１４−トリメチルペンタデカン−２−オン
EP2935178A1 (fr) * 2012-12-18 2015-10-28 DSM IP Assets B.V. Monoxyde d'azote à titre de catalyseur d'isomérisation cis/trans pour composés insaturés
JP6390048B2 (ja) * 2012-12-18 2018-09-19 ディーエスエム アイピー アセッツ ビー．ブイ．Ｄｓｍ Ｉｐ Ａｓｓｅｔｓ Ｂ．Ｖ． 組み合わされた不斉水素化によって特定の生成物を定量的に得るためのｅ／ｚ異性体の混合物の使用
CN107879914B (zh) * 2017-11-24 2020-11-20 万华化学集团股份有限公司 一种高效精馏柠檬醛制备橙花醛的方法及用于该方法的催化剂
CN111153765B (zh) * 2019-12-21 2020-10-20 南京汉欣医药科技有限公司 不同顺反异构体比例维生素k1及其中间体卤代植物醇的制备方法

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